JPH0424445B2 - - Google Patents

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Publication number
JPH0424445B2
JPH0424445B2 JP59109583A JP10958384A JPH0424445B2 JP H0424445 B2 JPH0424445 B2 JP H0424445B2 JP 59109583 A JP59109583 A JP 59109583A JP 10958384 A JP10958384 A JP 10958384A JP H0424445 B2 JPH0424445 B2 JP H0424445B2
Authority
JP
Japan
Prior art keywords
fibers
pitch
temperature
treated
fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59109583A
Other languages
Japanese (ja)
Other versions
JPS60259629A (en
Inventor
Seiichi Kamimura
Takao Hirose
Yoshiho Hayata
Masayoshi Sakamoto
Yoshio Kishimoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eneos Corp
Original Assignee
Nippon Oil Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Oil Corp filed Critical Nippon Oil Corp
Priority to JP10958384A priority Critical patent/JPS60259629A/en
Priority to US06/659,261 priority patent/US4574077A/en
Priority to DE8484307010T priority patent/DE3479139D1/en
Priority to EP84307010A priority patent/EP0148560B1/en
Publication of JPS60259629A publication Critical patent/JPS60259629A/en
Publication of JPH0424445B2 publication Critical patent/JPH0424445B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、ピツチ系黒鉛化繊維の製造方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing pitch graphitized fibers.

ピツチを原料として炭素繊維を製造する方法
は、原料が安価であり、また炭化収率が高いため
ポリアクリロニトリル系に比べ有利であり、さら
に紡糸後の不融化、炭化あるいは黒鉛化といつた
熱処理工程における処理時間を短くすることがで
きれば、ポリアクリロニトリル系に対する価格面
での優位性を一層明確にすることができる。
The method of producing carbon fiber using pitch as a raw material is advantageous compared to polyacrylonitrile systems because the raw material is inexpensive and the carbonization yield is high.It also has a heat treatment process such as infusibility, carbonization, or graphitization after spinning. If the treatment time can be shortened, the price advantage over polyacrylonitrile systems can be further clarified.

これまで、不融化処理時間を短縮するために各
種の触媒あるいは促進剤が検討され、金属塩、ア
ンモニウム塩、無機酸、ハロゲンなどが提案され
ているが、不融化促進効果あるいは最終製品であ
る炭素繊維の物性などからみて、満足なものは未
だ得られていない。例えば、ピツチ繊維を塩酸、
硫酸あるいは硝酸などの無機酸で接触処理したの
ち、不融化処理を行つた場合、不融化促進効果を
示すものもあるが、最終製品である炭素繊維の物
性を低下させてしまうという欠点がある。
Up to now, various catalysts or accelerators have been investigated to shorten the infusibility treatment time, and metal salts, ammonium salts, inorganic acids, halogens, etc. have been proposed. In terms of the physical properties of the fibers, satisfactory results have not yet been obtained. For example, Pituchi fiber is mixed with hydrochloric acid,
When infusibility treatment is performed after contact treatment with an inorganic acid such as sulfuric acid or nitric acid, some products exhibit an infusibilization promoting effect, but this has the disadvantage of reducing the physical properties of the final product, carbon fiber.

一方、ピツチ系黒鉛化繊維は、炭化繊維を不活
性ガス雰囲気下、2000〜3000℃で熱処理すること
により製造されている。ここでいう炭化繊維と
は、ピツチ繊維を酸化性ガス雰囲気下で処理する
ことにより得られる不融化繊維を、不活性ガス雰
囲気下800〜1300℃で熱処理することにより得ら
れるものであり、実質的に酸素を含有しない繊維
である。これらの不融化繊維の炭化は、通常、不
活性ガス中1〜30℃/分程度の速度で800〜1300
℃程度まで昇温することにより実施されており、
この際昇温速度を大きくすると繊維の強度の低下
を招くといわれている。しかしながらこの方法は
長時間にわたり高温を必要とするので生産性の低
下を招くのみならず経済上きわめて不利である。
On the other hand, Pitch-based graphitized fibers are produced by heat-treating carbonized fibers at 2000 to 3000°C in an inert gas atmosphere. The carbonized fibers referred to here are those obtained by heat-treating infusible fibers obtained by treating pitch fibers in an oxidizing gas atmosphere at 800 to 1300°C in an inert gas atmosphere, and are substantially It is a fiber that does not contain oxygen. Carbonization of these infusible fibers is usually carried out at a rate of 800 to 1300 °C in an inert gas at a rate of about 1 to 30 °C/min.
It is carried out by raising the temperature to about ℃,
At this time, it is said that increasing the temperature increase rate causes a decrease in the strength of the fibers. However, this method requires high temperatures for a long period of time, which not only leads to a decrease in productivity but is also economically disadvantageous.

すなわち、ピツチ系黒鉛化繊維の製造工程にお
いて、不融化、炭化および黒鉛化のいずれも時間
短縮が課題となつており、なおかつこの時間短縮
と製品物性の向上を両立させる焼成工程が必要と
されているのである。
In other words, in the production process of Pitch-based graphitized fibers, shortening the time for infusibility, carbonization, and graphitization is an issue, and there is a need for a firing process that simultaneously shortens this time and improves the physical properties of the product. There is.

本発明者らは鋭意研究の結果、炭素質ピツチを
溶融紡糸して得られるピツチ繊維をNO2を0.1〜
50vol%含有する酸化性ガス雰囲気下で処理して
窒素分を0.1〜5.0wt%含有する不融化繊維とし、
該不融化繊維を不活性ガス雰囲気下40℃/分以上
の速度で昇温し、2000〜3000℃で熱処理すること
により、焼成工程に要する時間を著しく短縮で
き、かつ優れた性能を有するピツチ系黒鉛化繊維
が得られることを見出したものである。
As a result of intensive research, the present inventors have found that pitch fibers obtained by melt spinning carbonaceous pitch contain NO 2 of 0.1 to 0.1%.
Processed in an oxidizing gas atmosphere containing 50 vol% to produce infusible fibers containing 0.1 to 5.0 wt% nitrogen,
By raising the temperature of the infusible fiber at a rate of 40°C/min or more in an inert gas atmosphere and heat-treating it at 2000 to 3000°C, the time required for the firing process can be significantly shortened, and the Pitch type has excellent performance. It was discovered that graphitized fibers can be obtained.

また、本発明者らは炭素質ピツチを溶融紡糸し
て得られるピツチ繊維をNO2を0.1〜50vol%含有
する酸化性ガス雰囲気下で処理して窒素分を0.1
〜5.0wt%含有する不融化繊維とした後、該不融
化繊維を不活性ガス雰囲気下450〜600℃で処理し
て実質的に酸素を含有する前炭化繊維とし、該前
炭化繊維を不活性ガス雰囲気下40℃/分以上の速
度で昇温し、2000〜3000℃で熱処理することによ
り、焼成工程に要する時間を著しく短縮でき、か
つ優れた性能を有するピツチ系黒鉛化繊維が得ら
れることを併せ見出したものである。
In addition, the present inventors treated pitch fibers obtained by melt spinning carbonaceous pitch in an oxidizing gas atmosphere containing 0.1 to 50 vol% NO 2 to reduce the nitrogen content to 0.1.
After forming infusible fibers containing ~5.0 wt%, the infusible fibers are treated at 450 to 600°C in an inert gas atmosphere to become pre-carbonized fibers that substantially contain oxygen, and the pre-carbonized fibers are inert. By increasing the temperature at a rate of 40°C/min or more in a gas atmosphere and heat-treating at 2000-3000°C, the time required for the firing process can be significantly shortened, and a pitch-based graphitized fiber with excellent performance can be obtained. This is what we found together.

以下の本発明を詳述する。 The invention will be described in detail below.

本発明に用いる炭素質ピツチとしてはコールタ
ールピツチ、SRCなどの石炭系ピツチ、エチレ
ンタールピツチ、デカントオイルピツチ等の石油
系ピツチあるいは合成ピツチなどの各種のピツチ
を包含するが、特に石油系ピツチが好ましい。
The carbonaceous pitch used in the present invention includes various pitches such as coal-based pitch such as coal tar pitch and SRC, petroleum-based pitch such as ethylene tar pitch and decant oil pitch, or synthetic pitch, but petroleum-based pitch is particularly suitable. preferable.

前記ピツチを変性したもの、例えばテトラリン
などの水素供与物で処理したもの、20〜350Kg/
cm2の水素加圧下に水素化したもの、熱処理により
改質したもの、溶剤抽出などの手段により改質し
たもの、あるいはこれらの方法を適宜組み合わせ
て改質したもの等の各種変性ピツチも本発明でい
う炭素質ピツチである。
The above pitch is modified, for example, treated with a hydrogen donor such as tetralin, 20-350 kg/
The present invention also covers various modified pitches, such as those hydrogenated under hydrogen pressure of cm2 , those modified by heat treatment, those modified by means such as solvent extraction, or those modified by an appropriate combination of these methods. This is carbonaceous pitch.

すなわち、本発明の炭素質ピツチとはピツチ繊
維を形成し得る前駆体ピツチを総称する意味に用
いられる。
That is, the carbonaceous pitch of the present invention is used to collectively refer to precursor pitches capable of forming pitch fibers.

本発明の炭素質ピツチは、光学的に等方性のピ
ツチであつてもよいし、また光学的に異方性のピ
ツチであつてもよい。
The carbonaceous pitch of the present invention may be an optically isotropic pitch or an optically anisotropic pitch.

光学的に等方性のピツチである場合、反射率が
9.0〜11.0%の範囲内の値を示すものが好ましい。
ここで反射率とは、アクリル樹脂等の樹脂中にピ
ツチを包埋せしめたのち研磨し、反射率測定装置
により空気中にて測定される。
When the pitch is optically isotropic, the reflectance is
Those exhibiting a value within the range of 9.0 to 11.0% are preferred.
Here, the reflectance is measured by embedding a pitch in a resin such as acrylic resin, polishing it, and measuring it in air using a reflectance measuring device.

光学的に異方性のピツチとは、ピツチを常圧も
しくは減圧下に窒素等の不活性ガスを通気しなが
ら通常340〜450℃にて加熱処理を行うことにより
得られる光学的異方性相を含有するピツチであ
り、特に光学的異方性の割合が5〜100%のもの
が好ましい。
Optically anisotropic pitch is an optically anisotropic phase obtained by heat-treating pitch, usually at 340 to 450°C, while passing an inert gas such as nitrogen under normal pressure or reduced pressure. It is particularly preferable to use a pitch containing an optical anisotropy of 5 to 100%.

本発明に用いる炭素質ピツチは軟化点が200〜
400℃のものが好ましく、240〜300℃のものが特
に好ましい。
The carbonaceous pitch used in the present invention has a softening point of 200~
A temperature of 400°C is preferred, and a temperature of 240 to 300°C is particularly preferred.

ピツチ繊維は前記炭素質ピツチを公知の方法に
て溶融紡糸を行うことにより得られる。例えば、
炭素質ピツチをその軟化点よりも30〜80℃高い温
度にて溶融し、直径0.1〜0.5mmのノズルから押し
出しながら100〜2000m/分で延伸することによ
りピツチ繊維を得る。
Pitch fibers can be obtained by melt spinning the carbonaceous pitch using a known method. for example,
Pitch fibers are obtained by melting carbonaceous pitch at a temperature 30 to 80° C. higher than its softening point, and drawing it at 100 to 2000 m/min while extruding it through a nozzle with a diameter of 0.1 to 0.5 mm.

次にピツチ繊維は、NO2を0.1〜50vol%含有す
る酸化性ガス雰囲気下にて不融化処理される。
NO2濃度は、好ましくは1〜10vol%、より好ま
しくは1〜5vol%である。
Next, the pitch fiber is infusible in an oxidizing gas atmosphere containing 0.1 to 50 vol% NO2 .
The NO 2 concentration is preferably 1 to 10 vol%, more preferably 1 to 5 vol%.

不融化処理時間は、5〜50分間、好ましくは10
〜30分間である。不融化時間が5分に満たない場
合には不融化が不十分であり、後段工程で繊維の
融着を招く。一方、不融化時間が50分を越える場
合には、工業的に不利となるばかりか、黒鉛化繊
維の物性の低下につながることもある。不融化反
応は不融化処理された繊維中の窒素分が0.1〜
5.0wt%、好ましくは0.2〜4.0wt%の範囲内にな
るよう行う。窒素分が前記範囲から外れる場合に
は、後記する不融化繊維あるいは前炭化繊維の40
℃/分以上での昇温が有効に行えず、得られる黒
鉛化繊維の物性が低下する。不融化処理は通常
400℃以下において行われ、好ましい処理温度は
150〜380℃であり、より好ましくは200〜350℃で
ある。処理温度が低すぎる場合には処理時間が長
くなり、また処理温度が高すぎる場合には、ピツ
チ繊維の融着あるいは消耗といつた現象を生ずる
ため好ましくない。昇温速度は1〜100℃/分、
好ましくは2〜50℃/分、より好ましくは5〜50
℃/分である。酸化性ガスとしては、通常、酸
素、オゾン、空気、硫黄酸化物、あるいはハロゲ
ン等の酸化性ガスを1種あるいは2種以上用い
る。本発明においては特に酸素、空気が好まし
い。
The infusibility treatment time is 5 to 50 minutes, preferably 10 minutes.
~30 minutes. If the infusibility time is less than 5 minutes, the infusibility is insufficient, leading to fusion of the fibers in the subsequent process. On the other hand, if the infusibility time exceeds 50 minutes, it is not only industrially disadvantageous, but also may lead to a decrease in the physical properties of the graphitized fiber. The infusibility reaction is performed when the nitrogen content in the infusible fiber is 0.1~
The content is adjusted to 5.0wt%, preferably within the range of 0.2 to 4.0wt%. If the nitrogen content is out of the above range, the
The temperature cannot be raised effectively at a rate of ℃/min or more, and the physical properties of the graphitized fiber obtained deteriorate. Infusibility treatment is usually
The preferred treatment temperature is 400℃ or below.
The temperature is 150 to 380°C, more preferably 200 to 350°C. If the treatment temperature is too low, the treatment time becomes long, and if the treatment temperature is too high, phenomena such as fusion or consumption of the pitch fibers occur, which is not preferable. The heating rate is 1 to 100℃/min.
Preferably 2-50°C/min, more preferably 5-50°C
°C/min. As the oxidizing gas, one or more of oxidizing gases such as oxygen, ozone, air, sulfur oxide, or halogen are usually used. In the present invention, oxygen and air are particularly preferred.

前記不融化繊維は、必要に応じて不活性ガス雰
囲気下450〜600℃で処理して実質的に酸素を含有
する前炭化繊維とすることができる。前炭化処理
は前記温度範囲内で実施され、その処理時間は限
定されないが、通常10秒〜1時間、好ましくは1
分〜10分である。また前炭化における昇温速度は
1℃/分〜2000℃/分、好ましくは4℃/分〜
1000℃/分である。
If necessary, the infusible fibers can be treated at 450 to 600° C. in an inert gas atmosphere to become pre-carbonized fibers that substantially contain oxygen. The pre-carbonization treatment is carried out within the above temperature range, and the treatment time is not limited, but is usually 10 seconds to 1 hour, preferably 1 hour.
Minutes to 10 minutes. In addition, the temperature increase rate in pre-carbonization is 1°C/min to 2000°C/min, preferably 4°C/min to
1000℃/min.

このようにして得られた不融化繊維あるいは前
炭化繊維を40℃/分以上の速度で昇温し不活性ガ
ス雰囲気下2000〜3000℃で熱処理することにより
黒鉛化繊維が得られる。本発明においては、不融
化繊維あるいは実質的に酸素を含有する前炭化繊
維を40℃/分以上の速度で2000〜3000℃の所定温
度まで昇温し、所定時間熱処理することにより高
強度のピツチ系黒鉛化繊維が得られるのであり、
実質的に酸素を含有しない、いわゆる炭化繊維
を、2000〜3000℃で熱処理しても得られる黒鉛化
繊維の強度は本発明の方法により得られる繊維に
は及ばない。ここでいう実質的に酸素を含有する
前炭化繊維とは、酸素を1〜40重量%、好ましく
は、3〜10重量%含有する繊維である。黒鉛化処
理時間は1秒〜1時間、好ましくは5秒〜10分間
である。黒鉛化温度までの昇温速度は40℃/分以
上、好ましくは100℃/分以上、更に好ましくは
500℃/分以上、最も好ましくは1000℃/分以上
である。
Graphitized fibers can be obtained by heating the thus obtained infusible fibers or pre-carbonized fibers at a rate of 40° C./min or more and heat-treating them at 2000 to 3000° C. in an inert gas atmosphere. In the present invention, infusible fibers or pre-carbonized fibers containing substantially oxygen are heated to a predetermined temperature of 2,000 to 3,000°C at a rate of 40°C/min or more, and heat-treated for a predetermined period of time to produce high-strength pitch fibers. As a result, graphitized fibers can be obtained.
Even if so-called carbonized fibers that do not contain substantially oxygen are heat-treated at 2000 to 3000° C., the strength of the graphitized fibers obtained by the method of the present invention is not as high as that of the fibers obtained by the method of the present invention. The pre-carbonized fibers substantially containing oxygen herein are fibers containing 1 to 40% by weight, preferably 3 to 10% by weight of oxygen. The graphitization treatment time is 1 second to 1 hour, preferably 5 seconds to 10 minutes. The heating rate to the graphitization temperature is 40°C/min or more, preferably 100°C/min or more, more preferably
The temperature is 500°C/min or more, most preferably 1000°C/min or more.

昇温速度が40℃/分未満の場合、あるいは不融
化繊維を一旦炭化繊維となし、炭化繊維を黒鉛化
する場合には優れた物性の黒鉛化繊維を得ること
ができない。
If the temperature increase rate is less than 40° C./min, or if the infusible fibers are first converted into carbonized fibers and then the carbonized fibers are graphitized, graphitized fibers with excellent physical properties cannot be obtained.

以下に実施例および比較例をあげ本発明を具体
的に説明するが、本発明はこれら実施例に制限さ
れるものではない。
EXAMPLES The present invention will be specifically explained below with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.

実施例 1 光学的異方性相を80%含有し、軟化点が280℃
である石油系前駆体ピツチを溶融紡糸し、平均糸
径13μのピツチ繊維を得た。このピツチ繊維を、
NO2を2vol%含有する酸素中、10℃/mmで30℃か
ら270℃まで昇温して24分間不融化処理を行つた。
処理後の繊維は窒素分2.4wt%を含有していた。
ついで100℃/mmで2500℃まで昇温し、2500℃で
10秒間黒鉛化したところ、得られた黒鉛化繊維
は、平均糸径10μ、弾性率60TON/mm2、引張り
強度330Kg/mm2であつた。
Example 1 Contains 80% optically anisotropic phase and has a softening point of 280°C
The petroleum precursor pitch was melt-spun to obtain pitch fibers with an average diameter of 13μ. This pitch fiber,
In an oxygen atmosphere containing 2 vol % of NO 2 , the temperature was raised from 30°C to 270°C at a rate of 10°C/mm to perform infusibility treatment for 24 minutes.
The treated fibers contained 2.4 wt% nitrogen.
Then, the temperature was increased to 2500℃ at 100℃/mm, and at 2500℃
When graphitized for 10 seconds, the graphitized fibers obtained had an average thread diameter of 10 μ, an elastic modulus of 60 TON/mm 2 and a tensile strength of 330 Kg/mm 2 .

比較例 1 実施例1の不融化繊維を、窒素中10℃/mmで昇
温して1000℃で30分炭化処理して炭素繊維を製造
した。得られた炭素繊維を2500℃で10秒間黒鉛し
たところ、得られた黒鉛化繊維は、平均糸径
10μ、弾性率55TON/mm2、引張り強度270Kg/mm2
であつた。
Comparative Example 1 The infusible fiber of Example 1 was heated in nitrogen at a rate of 10° C./mm and carbonized at 1000° C. for 30 minutes to produce carbon fiber. When the obtained carbon fibers were graphitized at 2500℃ for 10 seconds, the obtained graphitized fibers had an average yarn diameter of
10μ, elastic modulus 55TON/mm 2 , tensile strength 270Kg/mm 2
It was hot.

比較例 2 実施例1のピツチ繊維を、酸素中、10℃/mmで
270℃まで昇温して不融化処理し、ついで100℃/
mmで2500℃まで昇温し、2500℃で10秒間黒鉛化し
たところ、得られた黒鉛化繊維は、平均糸径
10μ、弾性率55TON/mm2、引張強度220Kg/mm2
あつた。
Comparative Example 2 The pitch fiber of Example 1 was heated at 10°C/mm in oxygen.
The temperature was raised to 270℃ for infusibility treatment, and then heated to 100℃/
When the temperature was raised to 2500℃ in mm and graphitized at 2500℃ for 10 seconds, the graphitized fibers obtained had an average yarn diameter of
10 μ, elastic modulus 55 TON/mm 2 , and tensile strength 220 Kg/mm 2 .

実施例1と比較例1および2との比較より、本
発明の方法により製造された黒鉛化繊維は、従来
法に比べすぐれた性能を有している。
A comparison between Example 1 and Comparative Examples 1 and 2 shows that the graphitized fiber produced by the method of the present invention has superior performance compared to the conventional method.

実施例 2 光学的異方性相を65%含有し、軟化点が252℃
である石油系前駆体ピツチを溶融紡糸し、平均糸
径11μのピツチ繊維を得た。このピツチ繊維を、
NO2を5vol%含有する空気中、5℃/mmで150℃
から290℃まで昇温して28分間不融化処理を行つ
た。処理後の繊維は窒素分0.3wt%を含有してい
た。ついで500℃で処理して前炭素繊維を製造し
た。得られた前炭素繊維は酸素を5重量%含有し
ており、これを1000℃/mmで2500℃まで昇温し、
2500℃で60秒間黒鉛化したところ、得られた黒鉛
化繊維は、平均糸径9μ、弾性率70TON/mm2、引
張り強度320Kg/mm2であつた。
Example 2 Contains 65% optically anisotropic phase and has a softening point of 252°C
The petroleum precursor pitch was melt-spun to obtain pitch fibers with an average diameter of 11μ. This pitch fiber,
150℃ at 5℃/mm in air containing 5vol% NO 2
The temperature was raised from 290°C to 290°C, and infusibility treatment was performed for 28 minutes. The treated fibers contained 0.3 wt% nitrogen. Then, it was treated at 500°C to produce a pre-carbon fiber. The obtained pre-carbon fiber contains 5% by weight of oxygen, which is heated to 2500°C at a rate of 1000°C/mm.
When graphitized at 2500° C. for 60 seconds, the graphitized fibers obtained had an average thread diameter of 9 μ, an elastic modulus of 70 TON/mm 2 and a tensile strength of 320 Kg/mm 2 .

実施例 3 反射率10.3%軟化点が270℃の光学的に等方性
の石油系前駆体ピツチを溶融紡糸し、平均糸径
12μのピツチ繊維を得た。このピツチ繊維を、
NO2を2vol%含有する空気中、5℃/mmで150℃
から300℃まで昇温して30分間不融化処理を行つ
た。処理後の繊維は窒素分0.8wt%を含有してい
た。ついで500℃で処理した前炭化繊維を製造し
た。得られた前炭化繊維の酸素含有率は4.5重量
%であつた。この前炭化繊維を50℃/分で2500℃
まで昇温し黒鉛化したところ、得られた黒鉛化繊
維の物性は弾性率65TON/mm2、引張り強度260
Kg/mm2であつた。
Example 3 An optically isotropic petroleum precursor pitch with a reflectance of 10.3% and a softening point of 270°C was melt-spun, and the average yarn diameter was
A 12μ pitch fiber was obtained. This pitch fiber,
150℃ at 5℃/mm in air containing 2vol% NO 2
The temperature was raised from 300°C to 300°C, and infusibility treatment was performed for 30 minutes. The treated fibers contained 0.8 wt% nitrogen. Pre-carbonized fibers were then processed at 500°C. The oxygen content of the obtained pre-carbonized fiber was 4.5% by weight. The carbonized fiber was heated to 2500℃ at 50℃/min.
The physical properties of the graphitized fiber obtained were an elastic modulus of 65 TON/mm 2 and a tensile strength of 260.
It was Kg/ mm2 .

実施例 4 実施例1におけるピツチ繊維をNO2を5vol%含
有する酸素中5℃/mmで130℃から280℃まで昇温
して30分間不融化処理を行つた。処理後の繊維は
窒素分1.8wt%を含有していた。ついで500℃で処
理して前炭化繊維を製造した。得られた前炭化繊
維の酸素含有率は6.0重量%であつた。この前炭
化繊維を3000℃/分で2500℃まで昇温し、2500℃
で30秒間処理したところ、得られた黒鉛化繊維の
物性は弾性率60TON/mm2、引張強度330Kg/mm2
あつた。
Example 4 The pitch fiber in Example 1 was heated in oxygen containing 5 vol % of NO 2 at a rate of 5° C./mm from 130° C. to 280° C. and subjected to infusibility treatment for 30 minutes. The treated fibers contained 1.8 wt% nitrogen. It was then treated at 500°C to produce pre-carbonized fibers. The oxygen content of the obtained pre-carbonized fiber was 6.0% by weight. Before this, the carbonized fiber was heated to 2500°C at 3000°C/min, and then heated to 2500°C.
When treated for 30 seconds, the physical properties of the graphitized fiber obtained were an elastic modulus of 60 TON/mm 2 and a tensile strength of 330 Kg/mm 2 .

実施例 5 実施例3における前炭化繊維を500℃/分で
2000℃まで昇温し、2000℃で1分間処理したとこ
ろ、弾性率は40TON/mm2、引張強度は200Kg/mm2
であつた。
Example 5 The pre-carbonized fiber in Example 3 was heated at 500°C/min.
When the temperature was raised to 2000℃ and treated at 2000℃ for 1 minute, the elastic modulus was 40TON/mm 2 and the tensile strength was 200Kg/mm 2
It was hot.

比較例 3 実施例1におけるピツチ繊維を、NO2を75vol
%含有する酸素中で、10℃/minで30℃から270
℃まで昇温して24分間不融化処理を行つた。処理
後の繊維は窒素分9vol%を含有していた。ついで
100℃/minで2500℃まで昇温し、2500℃で10秒
間黒鉛化したところ、得られた黒鉛化繊維は平均
糸径10μ、弾性率40ton/mm2、引張強度210Kg/mm2
であつた。
Comparative Example 3 Pitch fiber in Example 1 was mixed with 75vol of NO2 .
% oxygen at 10℃/min from 30℃ to 270℃
The temperature was raised to ℃ and the infusibility treatment was performed for 24 minutes. The treated fibers contained 9 vol% nitrogen. Then
When the temperature was raised to 2500℃ at 100℃/min and graphitized at 2500℃ for 10 seconds, the graphitized fibers obtained had an average thread diameter of 10μ, an elastic modulus of 40ton/mm 2 , and a tensile strength of 210Kg/mm 2
It was hot.

比較例 4 実施例1におけるピツチ繊維を、NO2
0.05vol%含有する酸素中で、10℃/minで30℃か
ら270℃まで昇温して24分間不融化処理を行つた。
処理後の繊維は窒素分0.1vol%を含有していた。
ついで100℃/minで2500℃まで昇温し、2500℃
で10秒間黒鉛化したところ、得られた黒鉛化繊維
は平均糸径10μ、弾性率43ton/mm2、引張強度230
Kg/mm2であつた。
Comparative Example 4 The pitch fiber in Example 1 was treated with NO 2
In an oxygen containing 0.05 vol%, the temperature was raised from 30°C to 270°C at 10°C/min for 24 minutes to make it infusible.
The treated fibers contained 0.1 vol% nitrogen.
Then, the temperature was increased to 2500℃ at 100℃/min, and then the temperature was increased to 2500℃.
When graphitized for 10 seconds at
It was Kg/ mm2 .

比較例 5 実施例2におけるピツチ繊維を、NO2
0.05vol%含有する空気中、5℃/minで150℃〜
290℃まで昇温して28分間不融化処理を行つた。
処理後の不融化繊維は窒素分0.05wt%を含有して
いた。ついで該不融化繊維を500℃で処理して前
炭化繊維を製造した。得られた前炭化繊維を1000
℃/minで2500℃まで昇温し、2500℃で60秒間黒
鉛化したところ、得られた黒鉛化繊維は平均糸径
9μ、弾性率41ton/mm2、引張強度220Kg/mm2であ
つた。
Comparative Example 5 The pitch fiber in Example 2 was treated with NO 2
150℃~ at 5℃/min in air containing 0.05vol%
The temperature was raised to 290°C and infusibility treatment was performed for 28 minutes.
The treated fibers contained 0.05 wt% nitrogen. The infusible fibers were then treated at 500°C to produce pre-carbonized fibers. The obtained pre-carbonized fiber is 1000
When the temperature was raised to 2500℃ at a rate of ℃/min and graphitized at 2500℃ for 60 seconds, the graphitized fibers obtained had an average thread diameter.
It had an elastic modulus of 9μ, an elastic modulus of 41 ton/mm 2 , and a tensile strength of 220 Kg/mm 2 .

比較例 6 実施例2におけるピツチ繊維を、NO2を75vol
%含有する空気中、5℃/minで150℃〜290℃ま
で昇温して28分間不融化処理を行つた。処理後の
不融化繊維は窒素分8wt%を含有していた。つい
で該不融化繊維を500℃で処理して前炭化繊維を
製造した。得られた前炭化繊維を1000℃/minで
2500℃まで昇温し、2500℃で60秒間黒鉛化したと
ころ、得られた黒鉛化繊維は平均糸径9μ、弾性
率42ton/mm2、引張強度190Kg/mm2であつた。
Comparative Example 6 Pitch fiber in Example 2 was mixed with 75vol of NO2 .
% in air, the temperature was raised from 150°C to 290°C at 5°C/min, and the infusibility treatment was performed for 28 minutes. The treated fibers contained 8 wt% nitrogen. The infusible fibers were then treated at 500°C to produce pre-carbonized fibers. The obtained pre-carbonized fiber was heated at 1000℃/min.
When the temperature was raised to 2500°C and graphitized at 2500°C for 60 seconds, the graphitized fibers obtained had an average thread diameter of 9μ, an elastic modulus of 42ton/mm 2 , and a tensile strength of 190Kg/mm 2 .

Claims (1)

【特許請求の範囲】 1 炭素質ピツチを溶融紡糸して得られるピツチ
繊維をNO2を0.1〜50vol%含有する酸化性ガス雰
囲気下で処理して窒素分を0.1〜5.0wt%含有する
不融化繊維とし、該不融化繊維を不活性ガス雰囲
気下40℃/分以上の速度で昇温し、2000〜3000℃
で熱処理することを特徴とするピツチ系黒鉛化繊
維の製造方法。 2 酸化性ガスが酸素、オゾン、空気、硫黄酸化
物またはハロゲンであることを特徴とする特許請
求の範囲第1項記載の方法。 3 炭素質ピツチを溶融紡糸して得られるピツチ
繊維をNO2を0.1〜50vol%含有する酸化性ガス雰
囲気下で処理して窒素分を0.1〜5.0wt%含有する
不融化繊維とした後、不活性ガス雰囲気下450〜
600℃で処理して実質的に酸素を含有する前炭化
繊維とし、該前炭化繊維を不活性ガス雰囲気下40
℃/分以上の速度で昇温し、2000〜3000℃で熱処
理することを特徴とするピツチ系黒鉛化繊維の製
造方法。 4 酸化性ガスが酸素、オゾン、空気、硫黄酸化
物またはハロゲンであることを特徴とする特許請
求の範囲第3項記載の方法。
[Claims] 1 Pitch fibers obtained by melt spinning carbonaceous pitch are treated in an oxidizing gas atmosphere containing 0.1 to 50 vol% of NO 2 to make them infusible to contain 0.1 to 5.0 wt% of nitrogen. The infusible fibers are heated at a rate of 40°C/min or more in an inert gas atmosphere to 2000 to 3000°C.
1. A method for producing pitch-based graphitized fiber, which is characterized by heat treatment. 2. The method according to claim 1, wherein the oxidizing gas is oxygen, ozone, air, sulfur oxide or halogen. 3 Pitch fibers obtained by melt-spinning carbonaceous pitch are treated in an oxidizing gas atmosphere containing 0.1 to 50 vol% NO 2 to make infusible fibers containing 0.1 to 5.0 wt% nitrogen, and then 450~ under active gas atmosphere
The pre-carbonized fibers are treated at 600°C to substantially contain oxygen, and the pre-carbonized fibers are heated at 40°C under an inert gas atmosphere.
A method for producing pitch-based graphitized fibers, which comprises raising the temperature at a rate of at least ℃/min and heat-treating at 2000 to 3000℃. 4. The method according to claim 3, wherein the oxidizing gas is oxygen, ozone, air, sulfur oxide or halogen.
JP10958384A 1983-10-14 1984-05-31 Production of graphitized pitch fiber Granted JPS60259629A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP10958384A JPS60259629A (en) 1984-05-31 1984-05-31 Production of graphitized pitch fiber
US06/659,261 US4574077A (en) 1983-10-14 1984-10-10 Process for producing pitch based graphite fibers
DE8484307010T DE3479139D1 (en) 1983-10-14 1984-10-12 Process for producing pitch-based graphite fibres
EP84307010A EP0148560B1 (en) 1983-10-14 1984-10-12 Process for producing pitch-based graphite fibres

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10958384A JPS60259629A (en) 1984-05-31 1984-05-31 Production of graphitized pitch fiber

Publications (2)

Publication Number Publication Date
JPS60259629A JPS60259629A (en) 1985-12-21
JPH0424445B2 true JPH0424445B2 (en) 1992-04-27

Family

ID=14513944

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10958384A Granted JPS60259629A (en) 1983-10-14 1984-05-31 Production of graphitized pitch fiber

Country Status (1)

Country Link
JP (1) JPS60259629A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62184125A (en) * 1986-02-10 1987-08-12 Toa Nenryo Kogyo Kk Production of carbon yarn and graphite yarn
JP2535590B2 (en) * 1988-02-05 1996-09-18 新日本製鐵株式会社 Method for producing mesophase pitch carbon fiber
JP2678384B2 (en) * 1989-06-09 1997-11-17 出光興産株式会社 Pitch for carbon fiber and method of manufacturing carbon fiber using the same
JPH0314624A (en) * 1989-06-09 1991-01-23 Idemitsu Kosan Co Ltd Production of carbon yarn
JP2825923B2 (en) * 1990-04-06 1998-11-18 新日本製鐵株式会社 High strength carbon fiber and precursor fiber
US5595720A (en) * 1992-09-04 1997-01-21 Nippon Steel Corporation Method for producing carbon fiber
JP2930166B2 (en) * 1992-09-04 1999-08-03 新日本製鐵株式会社 Carbon fiber production method
JP2930167B2 (en) * 1992-09-04 1999-08-03 新日本製鐵株式会社 Carbon fiber production method
JP3125062B2 (en) * 1993-02-24 2001-01-15 株式会社ペトカ Carbon fiber production method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112740A (en) * 1974-07-22 1976-01-31 Fujitsu Ltd MAIKUROPUROGURAMUNYORUKAUNTASEIGYOHOSHIKI
JPS5590621A (en) * 1978-12-26 1980-07-09 Kureha Chem Ind Co Ltd Production of carbon fiber

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112740A (en) * 1974-07-22 1976-01-31 Fujitsu Ltd MAIKUROPUROGURAMUNYORUKAUNTASEIGYOHOSHIKI
JPS5590621A (en) * 1978-12-26 1980-07-09 Kureha Chem Ind Co Ltd Production of carbon fiber

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